Catalytic cracking

Claim 2

In a process for the continuous cyclic fluid catalytic cracking of hydrocarbons with a zeolitic cracking catalyst in the absence of added hydrogen in a reaction zone to produce lower boiling hydrocarbons wherein cracking results in the deposition on the fluid cracking catalyst particles of a solid deposit of combustible hydrocarbons, the catalyst particles containing said deposit are regenerated in a regeneration zone by oxidation in the presence of air at elevated temperature to burn off said deposit, and the catalyst is recycled to said reaction zone where it is used to crack hydrocarbons in the absence of added hydrogen, the improvement which comprises cycling said particles of cracking catalyst through said reduction and regeneration zones in physical admixture with a minor amount relative to the quantity of said particles of cracking catalyst of fluidizable particles consisting essentially of calcined spray dried microspheres of kaolin clay impregnated with a minor amount of a platinum compound, said platinum compound being present in amount sufficient to promote the oxidation of carbon monoxide to carbon dioxide in a said regeneration zone, said impregnated microspheres having a low surface area as measured by the B.E.T. nitrogen absorption method.

Claim 3

In a process for the continous cyclic fluid catalytic cracking of hydrocarbons with a zeolitic cracking catalyst in the absence of added hydrogen in a reaction zone to produce lower boiling hydrocarbons wherein cracking results in the deposition on the fluid cracking catalyst particles of a solid deposit of combustible hydrocarbons, the catalyst particles containing said deposit are regenerated in a regeneration zone by oxidation in the presence of air at elevated temperature to burn off said deposit, and the catalyst is recycled to said reaction zone where it is used to crack hydrocarbons in the absence of added hydrogen, the improvement which comprises cycling said particles of cracking catalyst through said reaction and regeneration zones in physical admixture with particles of spray dried kaolin clay in the form of microspheres, said microspheres having been calcined at a temperature in the range of about 1000° to 2100° F., having a surface area, as measured by the B.E.T. nitrogen absorption method, in the range of about 10 to 15 m 2 /g., a pore volume, as measured by nitrogen absorption, in the range of about 0.02 to 0.04 cc./g. and a particle size distribution such that the particles are predominantly in the size range of 20 to 150 microns, said calcined microspheres having impregnated thereon a compound of platinum in amount sufficient to promote the oxidation of carbon monoxide to carbon dioxide in a regenerator for a fluid cracking catalyst, said particles of spray dried calcined clay impregnated with platinum being present in amount within the range of 30 to 5 parts by weight to 70 to 95 parts by weight of said particles of zeolitic aluminosilicate cracking catalyst.

Claim 4

In a process for the continous cyclic fluid catalytic cracking of hydrocarbons with a zeolitic cracking catalyst in the absence of added hydrogen in a reaction zone to produce lower boiling hydrocarbons wherein cracking results in the deposition on the fluid cracking catalyst particles of a solid deposit of combustible hydrocarbons, the catalyst particles containing said deposit are regenerated in a regeneration zone by oxidation in the presence of air at elevated temperature to burn off said deposit, and the catalyst is recycled to said reaction zone where it is used to crack hydrocarbons in the absence of added hydrogen, the improvement which comprises cycling said particles of cracking catalyst through said reaction and regeneration zones in physical admixture with particles of spray dried kaolin clay in the form of microspheres, said microspheres having been calcined at a temperature in the range of about 1000° to 2100° F., having a surface area, as measured by the B.E.T. nitrogen absorption method, in the range of about 10 to 15 m 2 /g., a pore volume, as measured by nitrogen absorption, in the range of about 0.02 to 0.04 cc./g. and a particle size distribution such that the particles are predominantly in the size range of 20 to 150 microns, said calcined microspheres having impregnated thereon a compound of platinum in amount sufficient to promote the oxidation of carbon monoxide to carbon dioxide in a regenerator for a fluid cracking catalyst, said particles of spray dried calcined clay impregnated with platinum being present in amount within the range of 30 to 5 parts by weight to 70 to 95 parts by weight of said particles of zeolitic aluminosilicate cracking catalyst.